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Publication numberUS3730959 A
Publication typeGrant
Publication dateMay 1, 1973
Filing dateJul 8, 1971
Priority dateJul 8, 1971
Publication numberUS 3730959 A, US 3730959A, US-A-3730959, US3730959 A, US3730959A
InventorsC Horres, R Leonard
Original AssigneeUs Interior
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Fabrication of high pressure seals for water equilibrated fiber bundles
US 3730959 A
Abstract
The formation of high pressure seals for water equilibrated, hollow fiber membranes is effected by injecting a solution of gelatin around the active membrane area, chilling the solution to solidify the gelatin and immobilize the water, washing the ends or inactive area of the membrane with warm water, drying the ends, and casting a seal on the solidified gelatin surface. The gelatin is removed by heating and washing the fibers.
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Description  (OCR text may contain errors)

Hori'es, Jr. et a1.

SUBSTlTUTE r012 MISSING XR s ATIcIIRooI/I III 0,730,959 [[451 ,May 1 1973 FABRICATION OF HIGH PRESSURE 2,757,439 8/1956 Burns .....264/3l7UX SEALS FOR WATER EQUILIBRATED 7 3,522,339 7/1970 Te Velde. ..264/261 X I FIBER BUNDLES I 1,082,231 12/1913 Nale ..264/26l X T Inventors: Charles Russell norm, In, Chapel OTHER PUBLICATIONS I i ggg Leonard Ralggh'l National I Academy of Sciences-National Research 0 0 I Council. Desalination Research Conference. [73] Assignecz The United States 01 America as Proceedings of the Conference on Desalination represented by the Secretary 01 the Research-Woods Hole, Mass, 14 June to 14 July Interior. I r I l96l.Hollow Fibers As Membranes for Reverse Osmosis" by Henry 1. Mahon, publication 942. 1963, pp; [-2] Filed. July 8,1971 345 348I I I I [21] Appl. No.: 160,668 Primary Examiner-Philip' E. Anderson 52 us. c1. ..264/263, 210/321, 264/265,

1 264/271, 264/317, 26 4/D1G. 44 Y 51 1m. (:1 ....B29d 3/02, B29d 27/00 [571 ABSTRACT [58] Field Of Search; ..264/41, 49, 221, The formation of high pressure seals for .water 1 6 4 l equilibrated, hollow fiber membranes is effected by in- 210/321 jecting a solution of gelatin around the active membrane area, chilling the solution to solidify the gelatin 1 I 'Ikeffl'ences Cited and immobilize the water, washing the ends or inactive area of the membrane with warm water, drying I UNITED STATES PATENTS the ends, and casting aseal on the solidified gelatin 3,422,008 1/1969 McLain ,J. ..2'10/22 surface. The gelatin is removed by heating and wash- 3 7()4.223 11/1972 Dietzsch et a1. ....210/321 X ing the fibers.

.551 3 1 12/1970 Cescon et a1. ..264/4l X 2,694,228 11/1954. Mathis ..264/317 X 12 Claims, 3Drawing Figures I II llI'I'I SURROUND FIBER \IVITH GELATIN SOLUTION I I I I SYEP 4 i g f t .T CAST,PLUS a ry ab CURE SEALANT Pate-mama, 1, 1973; f R 3,730,959

I I :2 Sha na- Shut 1 i .-.s.'-f." ti'fxrm R I I I l A :11! Va R was" auo onv nun suns STEP l,

SURROUND FIBER WiTH 575p 2 GELATIN SOLUTION CHILLHGELATIN F/GJ 2 v 7 STEP 5 STEP '4 REMOVE GELATIN CAST,PLUS CURE, SEALANT INVENTORS CHARLES RUSSELLHORRES RICHARD 1., LEONARD ATTORNEY l FABRICATION or area PRESSURE SEALS FOR I WATER EQUILIBRATED FIBER nunnws BACKGROUND,

One of the mostpromising techniques for the commercial desalination of saline waters, reverse osmosis is, as its name implies, the opposite of another process. Osmosis is a naturally occurring phenomenon in which solvent from a d lute Solu on pa r g H) tion ofseals in other systems with similar problems.

The usual methodof forming the seals on the end of a hollow fiber membrane bundle'is shown, for example,

brane into a more concentrated solution. This flow will continue unless opposed by a pressure equal in force to the" characteristic osmotic, pressure of the system. ln reverse osmosis, therefore, the flow of solvent is completely reversed by applying a pressure greater .than osmotic to the concentrated solution. Thus, by

contacting an appropriatemembrance with saline water under sufficient pressure, 'pure water will be forced through the membrane and recovered on the opposite side.

Obviously, the key to this process is in finding a membrane which demonstrates normal osmosis with respect to the solution to be separated. Thus, reverse osmosis was not known as amethod for desalinating aqueous sodium chloride solutions until late in the 1950's when itwas discovered that cellulose acetate allowed the passage of water from a dilute solution to a more concentrated one while prohibiting the flow of salt. Since that time new methodsof forming cellulose acetate membranes and new membrane materials have been discovered in an attempt to find a commercially acceptable membrane.

To be economical a reverse osmosis membrane must meet the requirements of adequate selectivity and water flux. Selectivity refers to the relative ability of the membrane to permit the flow of solvent while rejecting the passage of salt. The ideal membrane would v completely prohibit the flowof salt. Naturally, even with a membrane of perfect selectivity, the process will not be economical if pure water merely trickles through it. The second requirement of adequate flux,

. therefore, refers to the quantity of pure water flowing through a unit area of the membrane in a certain leaks in the system, membrane seals separating the high pressure areas from thecollection zones are critical in all reverse osmosis-desalination systems. The formation of seals around the'ends of the many little fibers used in a a hollow fiber bundle has created special problems. It is in U.S."Pat. No. 3,442,389 to M cLain. A mold is placed around the ends of the hollow fibers and a solidifiable material such as epoxy resin is poured around these ends. After the resin hardens, a cross sectional cut may amount of time. Research to date has been effective in.

economic savings. Some of the most promising-com-- mercial systems use bundles of-membranes formed into tiny hollow fibers, typically with outside diameters of from 50 to 40 microns and with wall thickness to tliamctcr ratios of from ().l5 to 0.35. These fibers resent a tremendously large membrane surface area er volume of equipment and thus, even if the flux or flow per area of the membrane is not the best, the rate of recovery of pure water from the system may be least be acceptable. Although desalination systems using bundles of'hollow fibers may actually be used in many specific different designs, the usual one will have the saline water pressurized from about l5 to L500 psi or more on the outside of the hollow fibers. Pure water moves through the membrane surfaces and is channeled by the fibers to collection means outside the desalination area.

be partially or completely. impaired. Most membrane be made through the resin and mold to expose the fiber ends. I

As mentioned in the patent, in order to form an ef fective seal it is necessary to use a sealant which is fluid enough to completely surround and encapture all the fiber 'ends in the closely packed bundle. The patent, however, acknowledges that if the sealant is very fluid, there is a tendency for wicking" to occur. In this phenomenon sealant creeps along the'fibers particu larly in channels formed between parallel fibers and out onto the active portions of the membrane. Activeportion" refers to that partof the membranefiber through' which reverse osmosis and, desalination is effected as opposed to the inactive'portions around which the seal isformed and which extend beyond the seal to the product collection means. Unfortunately, sealant which wicks onto the active surfaces hardens there and deadens these active areas. 7

US. Pat. No. 3,442,002 to Geary et al'. shows one solution to'the problem o fwicking centrifugal casting of'the seal. By rotating the fiber bundle during casting and curing of the membrane a centrifugal force is applied outwardly away from the active areas thereby offsetting the forces which cause wicking to occur.

Although the method of Geary et almay be effective in preventing wicking and localized deadening of active membrane surfaces, the membrane surfaces may still materials are water equilibrated and from the time of theirformation to their use they are kept in contact with water; this is particularly true of membranes of celluloseacetate and other cellulose derivatives. However, a problem exists since a satisfactory sealant for high pressure use has not been found for wet fibers. Either the moisture in and on the fiber is not compatible with the sealant, terminating cure, or the bond formed is not strong enough to prevent separation from the fiber as it'drie's during curing. Attempts to form seals while drying only the ends of the fibers have failed because water wicks from the other membrane areas Because of the high pressures employed and the contamination of product water which might be caused by into the seal. Unfortunately, allowing the membranes to be driedand to remain'dryingduring casting and these problems and it'is an objectof our invention to improve the niethodof forming seals on the end of hollow fiber waterequilibrated'revrse osmosis membranes. v

More generally, it is an object of our invention to improve the method of forming seals where the wicking" of sealant from the area being sealed or the wicking of liquids into the seal may present problems.

It is also a general object of our invention to improve the method of forming seals whenever the areas outside the seal are water equilibrated.

The basic steps of our process will be described in the following specification and are illustrated in FIG. 1 showing the formation of a seal on a hollow fiber bundle.

FIG. 2 illustrates a typical hollow fiber bundle and seal formed by the process and suitable for use in the reverse osmosis desalination apparatus shown in FIG. 3.

INVENTION We have now found a method for avoiding the previous disadvantages of forming seals for water equilibrated hollow fiber membranes. The essence of the invention is that a distinct separation is formed between dry and wet fiber regions so that the properties of the active membrane areas are not impaired when the inactive membrane regions are dried for seal formation. This result is achieved by surrounding the active fiber areas with a water immobilizing gel and thereafter forming the seal on the dry inactive fiber region.

This process is illustrated in FIG. 1. A bundle of looped membrane fibers 1 are placed in an appropriate container such as a tube or cylinder 3 such that all the.

fiber ends 2 are exposed. A warm aqueous solution of 4 gelatin or other water immobilizing material 4 is then poured into the container to surround the active membrane surfaces. Thus, the container is filled to a level such that all membrane surfaces that will be in contact with saline solution when the membranes are in operation will be covered by gelatin.

In step 2 the aqueous gelatin solution is chilled to solidify the gelatin 4 and immobilize the water surrounding the active membrane area. This may be accomplished, for example, by immersing the container 3 in an ice bath 5 at least up to the level of the solution in v the container. The gel solution is continuously chilled and kept in a solid state until after the seal has been cast and has cured.

Following the solidification 0f the aqueous gelatin solution, the fiber ends 2 are prepared for sealing. This preparation will most likely consist of washing the ends with warm water to remove any gelatin solution which has wickcd into these ends and then drying them for a sufficient time to insure that the casting and curing of the seal will not be impaired by retained water. The drying may be accomplished with either air or some inert atmosphere such as nitrogen, carbon dioxide or other gaseous media. While it is essential that the membrane ends are thoroughly dried before casting of the seal, extreme drying conditions should be avoided to prevent the ends from becoming brittle.

In step 4 the seal around the fiber ends is prepared. This may be accomplished, for example, by surrounding the fiber ends with a cylindrical mold 7, which is pressed into the surface of the gelatin. Subsequently, an epoxy resin or other suitable sealant is poured into the mold onto the solidified gelatin surface so that each fiber end is encaptured in resin. Any suitable epoxy resin or. other sealant'known in the art may be used such as those shown in U. S. Pat. No. 3,422,008 herein incorporated by reference. The fiber ends 2 extend beyond the sealant.

When this sealant has hardened, the solidified gelatin is removed from around the active membrane surfaces. This may be accomplished by warming the gelatin, removing the gelatin and fibers from the container, and washing the fibers to remove adhered traces of gelatin.

The membrane is then ready for use although it may be stored with at least the active membrane areas immersed in water. The hollow fiber bundle and attached seal 8 of hardened epoxy resin is shown in its finished form in step 5.

FIGS. 2 and 3 show how a hollow fiber membrane bundle and attached seal formed by our process could be used to desalinize water by reverse osmosis. The apparatus consists of a hollow tube 100 to which T joints I01 and 102 are attached at either end.

The membrane element 111 consists of hollow fiber membrane bundle 108 which is looped around the top of a support rod 107 such that all ends 110 of the fibers are held by a seal at the base of the support rod. The seal 109 consists of a length of stainless steel tubing in which the fibers are sealed with epoxy. The sealing is accomplished as previously discussed with the exception that the support rod is also included.

The membrane element is then positioned inside tube 100 as shown in the partial section of FIG. 3 and is held in place in T-joint 1 02 by pressure fitting 112 through which fiber ends 110 project.

In operation saline water under a pressure greater than osmotic is pumped into the tube through fitting 103. In tube 100 the saline water is purified by reverse osmosis-the membrane material selectively allowing water to pass through and enter the hollow fibers while excluding salt. Product water is then recovered as it drains from the ends 110 of the hollow fibers. Brine, more concentrated in salt than the feed saline water, leaves the tube by fitting 104. The final pressure fitting 1-05 opens to pressure gauge 106 by which the process can be monitored.

The apparatus used in FIG. 3 is merely illustrative of one system utilizing reverse osmosis membranes and the seals formed by our invention. It is apparent that the actual design of the membrane system could take many forms.

We expect that our invention can be used advantageously to form seals in systems with similar problems. For example, where a water equilibrated membrane is in a configuration where wicking is not a problem (ex. a single large diameter tube), it may still be desirable to surround the active membrane area with a water immobilizing gel during casting to protect these surfaces from the effects of drying. Similarly,

, wicking may be a problem in some situations in which hrane with a solidifiable materialand then casting the seal on the solidified material. While we have used a solution of gelatin as this solidifiable material, we also expect that other materialssu'ch aspolyglycols, agar solutions, or solutions of sodium silicates, commonly referred 'toas water glass could be used.

Finally, the reverse osmosis membranes which may be sealed by our process should not be limited to those which may be used for desalination, but include others suitable for usein the separation of water from electrolyte solutions including sea water, brackish water,

acid mine water, and industrial brines and bittems; the

About 10 inches of fiber remained exposed at the other end. A warm aqueous gelatin solution (2.8 wt. percent) drying the exposed end of said fiber, and casting a solidifiable sealant resin upon said water immobilizing gel so as to completely surround and 'encapture the dry inactive portion of said fiber membrane. I '2.--The process of claim 1 equlibrated hollow fiber is a reverse osmosis membrane.

. 3. The process of claim 1 wherein said water immobili'zing gel is solidified gelatin solution.

4. The process of claim 1 wherein said solidifiable sealant is epoxy resin.

5. The' process of claim l'wherein said water equlibrated hollow fiber membrane is.a plurality of water equlibrated-hollow fiber membranes.

6. The process of claim 5 wherein said plurality of Y water equlibrated-hollow fibermembranes are reverse was pumped into the pipe and then chilled to solidify the gelatin. The exposed fiber ends were washed with hot water to remove traces of gelatin which wicked before solidifying, and the fiber ends were'then dried in warm air while continuing to chill the gelatin. Finally, an epoxy sealant was cast onto the hardened gelatin layer with the seal mold surrounding the pipe. Afterthe' seal cured. the threaded fitting was detached and the I. In a process for the manufacture of a high pressure 7 seal molded around a water equilibrated hollow fiber osmosis membranes.

7. The processfof claim 6 wherein said plurality of 'water equlibrated hollow fiber membranes are reverse osmosis membranessuitable for use in water desalination. i

"8. A process for the formation of a high pressure seal around theend of a water-equlibrated hollow fiber membrane comprising:

surrounding the active area of said fiber with an aqueous solution of gelatin,

chilling said solution to solidify said gelatin,

washing the-exposed end of said fiber to remove any gelatin or aqueous solution,

drying said exposed end of said hollow fiber,

casting a solidifiable sealant resin around said end of said fiber nd adjacent said solidified gelatin solui curingsaid solidifiable sealant and a removing said solidified gelatin solution from around 7 said active fiber area. 9. The process of claim 8 wherein said water equlibrated hollow fiber is a reverse osmosis. membrane.

10. The process of claim 8 wherein said resin is epoxy resin.

ll. The process of claim 8 wherein said water equlibrated hollow fiber membrane is a plurality of water equlibrated hollow fiber membranes.

12. The process of claim 11 wherein said plurality of water equlibrated hollow fibers are reverse osmosis membranes, suitable for use in water desalination.

wherein said water

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1082231 *Mar 26, 1913Dec 23, 1913E J HudnallMethod of setting tiles, bricks, and mosaics.
US2694228 *May 16, 1950Nov 16, 1954Clark A MathisMethod of making display assemblies
US2757439 *Feb 25, 1955Aug 7, 1956Raytheon Mfg CoTransistor assemblies
US3422008 *Oct 24, 1963Jan 14, 1969Dow Chemical CoWound hollow fiber permeability apparatus and process of making the same
US3522339 *Aug 1, 1966Jul 28, 1970Philips CorpMethod of making electrical monograin layer
US3551331 *Sep 22, 1969Dec 29, 1970Du PontReverse osmosis separations using a treated polyamide membrane
US3704223 *Jun 6, 1969Nov 28, 1972Dietzsch Hans JoachimDialysis apparatus with capillary exchanger
Non-Patent Citations
Reference
1 *National Academy of Sciences National Research Council. Desalination Research Conference. Proceedings of the Conference on Desalination Research. Woods Hole, Mass., 14 June to 14 July 1961. Hollow Fibers As Membranes for Reverse Osmosis by Henry I. Mahon, publication 942. 1963, pp. 345 348.
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3884814 *Jul 23, 1973May 20, 1975Rhone Poulenc SaApparatus for fractionating fluids
US3961010 *Jun 28, 1973Jun 1, 1976Serck Industries LimitedMethod of manufacturing heat exchangers
US3962766 *May 31, 1974Jun 15, 1976Pont-A-Mousson S.A.Process for assembling tubes of plastics material and assemblies resulting from said process
US3987142 *Sep 27, 1974Oct 19, 1976Lewis Woolf Griptight LimitedLatex dip process
US4038190 *May 29, 1974Jul 26, 1977Rhone-Poulenc S.A.Fluid fractionation apparatus and method of manufacturing the same
US4049765 *Apr 26, 1976Sep 20, 1977Nippon Zeon Co., Ltd.Method for setting end portion of bundle of thread-like bodies
US4061522 *Feb 3, 1977Dec 6, 1977International Telephone And Telegraph CorporationMethod and apparatus for terminating a fiber optic bundle
US4098852 *May 1, 1975Jul 4, 1978Rhone-Poulenc, S.A.Process for carring out a gas/liquid heat-exchange
US4105731 *Jul 1, 1977Aug 8, 1978Nippon Zeon Co., Ltd.Method of embedding an end of a bundle of thread-like bodies in a molding material and controlling capillary action by said material
US4138460 *Jun 10, 1977Feb 6, 1979Cordis Dow Corp.Method for forming tubesheets on hollow fiber tows and forming hollow fiber bundle assemblies containing same
US4252765 *Jan 16, 1980Feb 24, 1981Brumfield Robert CMethod for fabricating wound hollow fiber dialysis cartridges
US4568366 *Aug 30, 1983Feb 4, 1986Baxter Laboratories, Inc.In-line filter
US6592759May 3, 2001Jul 15, 2003Zenon Environmental Inc.Gel potting method and method to reduce twinning for filtering hollow fiber membranes
US6685832Jun 13, 2002Feb 3, 2004Zenon Environmental Inc.Method of potting hollow fiber membranes
US6964741Mar 3, 2003Nov 15, 2005Zenon Environmental Inc.Apparatus for withdrawing permeate using an immersed vertical skein of hollow fiber membranes
US7022231Jan 30, 2004Apr 4, 2006Zenon Environmental Inc.Apparatus incorporating potted hollow fiber membranes
US7063788Feb 26, 2003Jun 20, 2006Zenon Environmental Inc.Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US7087173May 10, 2004Aug 8, 2006Zenon Environmental Inc.for immersed membranes; to scour the membranes and to disperse areas of tank water having increased concentrations of rejected solids from near the membranes; minimum energy use, cost and maintenance required to keep the aerators from plugging
US7534353Sep 19, 2006May 19, 2009Zenon Technology Partnershipbubbles of a fiber-cleansing gas ("scrubbing gas") flowing parallel to fibers in a vertical skein are more effective than bubbles which are intercepted by arcuate fibers crossing the path of the rising bubbles
US7537701Dec 17, 2007May 26, 2009Zenon Technology PartnershipMembrane filtration module with adjustable header spacing
US7615157Feb 17, 2005Nov 10, 2009Zenon Technology PartnershipApparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US7708888Sep 19, 2006May 4, 2010Zenon Technology PartnershipApparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US8075776Feb 4, 2005Dec 13, 2011Zenon Technology PartnershipApparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes
US8133344Jul 5, 2007Mar 13, 2012Asahi Kasei Chemicals CorporationProcess for production of hollow-fiber membrane bundles
USRE39294Oct 11, 2001Sep 19, 2006Zenon Environmental Inc.Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
USRE42669Jul 20, 2000Sep 6, 2011Zenon Technology PartnershipVertical cylindrical skein of hollow fiber membranes and method of maintaining clean fiber surfaces
EP0044075A1 *Jul 14, 1981Jan 20, 1982Toyo Boseki Kabushiki KaishaFluid separation element
EP0163900A2 *Apr 23, 1985Dec 11, 1985Mitsubishi Rayon Co., Ltd.Hollow-fiber filter module
EP0207379A1 *Jun 19, 1986Jan 7, 1987Mitsubishi Rayon Co., Ltd.Hollow-fiber filter module and filtration method using the same
EP1213048A1Aug 8, 1996Jun 12, 2002Zenon Environmental Inc.Method of potting fiber membranes
EP2042228A1 *Jul 5, 2007Apr 1, 2009Asahi Kasei Chemicals CorporationProcess for produciton of hollow-fiber membrane bundles
WO2001085315A1 *May 2, 2001Nov 15, 2001Marshal DeaneGel potting method for producing filtering hollow fibre membranes
WO2003086591A1 *Apr 16, 2003Oct 23, 2003Christoph KullmannMethod for the production of a header comprising a fiber bundle made of open-ended capillary membranes
WO2005046847A1 *Oct 17, 2003May 26, 2005Christoph KullmannMethod for producing a head piece comprising a fibre bundle consisting of open-ended capillary membranes
Classifications
U.S. Classification264/263, 210/321.9, 264/265, 385/143, 264/317, 264/DIG.440, 210/500.23
International ClassificationB01D63/02
Cooperative ClassificationY10S264/44, B01D63/024, B01D63/022
European ClassificationB01D63/02B10, B01D63/02D